Catalytic reaction process
US-2024173711-A1 · May 30, 2024 · US
US11241674B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11241674-B2 |
| Application number | US-201916356856-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 18, 2019 |
| Priority date | Mar 20, 2018 |
| Publication date | Feb 8, 2022 |
| Grant date | Feb 8, 2022 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention relates to catalyst product, a method of making a catalyst and its use in fluid catalytic conversion process. In particular, this invention relates to a process for the preparation of CO-combustion promoter microspheres, comprising a large crystallite low surface area alumina; a composite binder comprising nano-crystallite alumina and dispersant; and platinum or palladium or both. The large crystallite low surface area alumina is bound together by the composite binder in the said particulate composition.
Opening claim text (preview).
The invention claimed is: 1. A process for preparation of a particulate CO oxidation promoter catalyst composition, the process comprising: (a) reacting a nano-crystallite alumina with a dispersant to obtain a composite binder; (b) milling and homogenizing a large crystallite low surface area alumina with the composite binder to obtain a precursor slurry, wherein the large crystallite low surface area alumina has a crystallite size in a range of 4.5 to 40 nm and a surface area in a range of 20 to 150 m 2 /g; (c) spray drying the precursor slurry to obtain a particulate green catalyst; (d) calcining the green catalyst to obtain a calcined alumina support; and (e) impregnating the calcined alumina support with at least one of platinum or palladium to obtain the particulate CO oxidation promoter catalyst composition. 2. The process as claimed in claim 1 , wherein the dispersant is selected from a group consisting of at least one of aluminum hydroxyl chloride and aluminum hydroxynitrate. 3. The process as claimed in claim 1 , wherein the composite binder comprises of the nano-crystallite alumina in a range of 1 to 35 wt % and the dispersant in a range of 0.1 to 10 wt %. 4. The process as claimed in claim 1 , wherein the nano-crystallite alumina has a crystallite crystallize size in a range of 2 to 5 nm and a surface area in a range of 150-430 m 2 /g. 5. The process as claimed in claim 1 , wherein the nano-crystallite alumina has a pseudo-boehmite phase. 6. The process as claimed in claim 1 , wherein the particulate CO oxidation promoter catalyst composition has a shape of a microsphere. 7. A particulate CO oxidation promoter catalyst composition, prepared according to the process as claimed in claim 1 , the composition comprising: (a) a large crystallite low surface area alumina, wherein the large crystallite low surface area alumina has a crystallite size in a range of 4.5 to 40 nanometer and a surface area in a range of 20 to 150 m 2 /g; (b) a composite binder comprising nano-crystallite alumina and a dispersant; and (c) platinum, palladium, or both; wherein, the large crystallite low surface area alumina is bound together by the composite binder in the particulate CO oxidation promoter catalyst composition. 8. The composition as claimed in claim 7 , wherein the particulate CO oxidation promoter catalyst composition has an average pore diameter in a range of 60 Å to 600 Å, a surface area in a range of 40 to 160 m 2 /g, ABD (apparent bulk density) in a range of 0.75 to 1.00 g/cc, and ASTM D5757 attrition index below 10. 9. The composition as claimed in claim 7 , wherein the nano-crystallite alumina has a crystallite size in a range of 2 to 5 nanometer and a surface area in a range of 150 to 430 m 2 /g. 10. The composition as claimed in claim 7 , wherein the composition comprises: (a) 35 to 95 wt. % of the large crystallite low surface area alumina; (b) 2 to 45 wt % of the composite binder comprising 1 to 35 wt % nano-crystallite alumina and 0.1 to 10 wt % dispersant; and (c) 100 to 1000 ppm of platinum, palladium, or both. 11. The composition as claimed in claim 7 , wherein the large crystallite low surface area alumina is selected from a group consisting of bayerite, boehmite, pseudoboehmite, gamma, alpha, delta, and theta. 12. The composition as claimed in claim 7 , wherein the nano-crystallite alumina is selected from a group consisting of pseudo-boehmite and boehimite.
Related publications grouped by family.
Answers are generated from the same data shown on this page.